US20180187566A1 - Seal arrangement in a turbine and method for confining the operating fluid - Google Patents
Seal arrangement in a turbine and method for confining the operating fluid Download PDFInfo
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- US20180187566A1 US20180187566A1 US15/738,304 US201615738304A US2018187566A1 US 20180187566 A1 US20180187566 A1 US 20180187566A1 US 201615738304 A US201615738304 A US 201615738304A US 2018187566 A1 US2018187566 A1 US 2018187566A1
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Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D11/00—Preventing or minimising internal leakage of working-fluid, e.g. between stages
- F01D11/003—Preventing or minimising internal leakage of working-fluid, e.g. between stages by packing rings; Mechanical seals
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D11/00—Preventing or minimising internal leakage of working-fluid, e.g. between stages
- F01D11/02—Preventing or minimising internal leakage of working-fluid, e.g. between stages by non-contact sealings, e.g. of labyrinth type
- F01D11/04—Preventing or minimising internal leakage of working-fluid, e.g. between stages by non-contact sealings, e.g. of labyrinth type using sealing fluid, e.g. steam
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D25/00—Component parts, details, or accessories, not provided for in, or of interest apart from, other groups
- F01D25/08—Cooling; Heating; Heat-insulation
- F01D25/12—Cooling
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D25/00—Component parts, details, or accessories, not provided for in, or of interest apart from, other groups
- F01D25/16—Arrangement of bearings; Supporting or mounting bearings in casings
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D25/00—Component parts, details, or accessories, not provided for in, or of interest apart from, other groups
- F01D25/18—Lubricating arrangements
- F01D25/183—Sealing means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D25/00—Component parts, details, or accessories, not provided for in, or of interest apart from, other groups
- F01D25/32—Collecting of condensation water; Drainage ; Removing solid particles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16J—PISTONS; CYLINDERS; SEALINGS
- F16J15/00—Sealings
- F16J15/16—Sealings between relatively-moving surfaces
- F16J15/34—Sealings between relatively-moving surfaces with slip-ring pressed against a more or less radial face on one member
- F16J15/3464—Mounting of the seal
- F16J15/348—Pre-assembled seals, e.g. cartridge seals
- F16J15/3484—Tandem seals
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16J—PISTONS; CYLINDERS; SEALINGS
- F16J15/00—Sealings
- F16J15/16—Sealings between relatively-moving surfaces
- F16J15/40—Sealings between relatively-moving surfaces by means of fluid
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
- F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
- F05D2220/00—Application
- F05D2220/30—Application in turbines
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
- F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
- F05D2240/00—Components
- F05D2240/55—Seals
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
- F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
- F05D2240/00—Components
- F05D2240/60—Shafts
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
- F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
- F05D2260/00—Function
- F05D2260/20—Heat transfer, e.g. cooling
Definitions
- the present invention relates to a seal arrangement in a turbine working in an Organic Rankine Cycle (ORC), and a method for confining the operating fluid in the turbine.
- ORC Organic Rankine Cycle
- ORC Organic Rankine Cycle
- ORC Organic Rankine Cycle has been used also to denote cycles with changes of state from liquid to gaseous and vice versa, even with operating fluids other than water, though not “organic” in the strict sense of “containing carbon”. For example, ammonia and nitrogen oxides are fluids having these characteristics.
- thermodynamic cycle in order to generate the heat required for vaporizing the organic operating fluid, biomass or waste heats of industrial processes is often used.
- the operating fluid is expanded in a turbine generally connected to an electric generator for producing electric power.
- the organic operating fluid In most of the Rankine cycle ORC plants, the organic operating fluid must necessarily remain confined in the plant, in order to prevent atmosphere contaminations. On the other hand, air must be prevented from entering the thermodynamic cycle, because oxygen would contribute to oxidation and corrosion of the organic operating fluid and, furthermore, the humidity in the air would pollute the operating fluid.
- FIG. 1 shows a classic solution according to the known art: the turbine 1 ′ and generator 2 ′ are directly coupled to each other and isolated inside a casing 3 ′.
- the shaft 4 ′ of the turbine 1 ′ and the generator 2 ′ both rotate within the same volume defined by the volute 3 ′ in which there is the operating fluid.
- the shaft 4 ′ of the turbine does not cross the wall of the casing 3 ′ thereby limiting only to the stationary seal the risk of leakages of the operating fluid.
- Electric power produced by the generator is transmitted to the outside through convenient electrical connectors 5 ′ constrained to the volute 3 ′ and being obviously fluid tight, to which corresponding cables can be connected.
- This solution suffers from the drawback of exposing the electric generator to the operating fluid. As the insulation of electric windings of the generator 2 ′ are continuously in contact with the operating fluid, in the long run it can be damaged and impaired.
- FIG. 2 shows an evolution of the previous solution, still according to the known art.
- the stator part and the rotor part of the generator are kept fluidically separated by a cylindrical partition 6 ′, named liner, and gaskets 7 ′.
- bearings 8 ′ (schematically shown) supporting the shaft 4 ′ are exposed to the operating fluid, therefore the latter having to act also as lubricant and cooling fluid.
- the operating fluid is discharged through suitable ducts.
- radial and axial magnetic bearings have been proposed.
- FIG. 3 shows one of the configurations provided by the regulation: it is a configuration called “Double seal” or “Tandem seal” of “back to back” type, particularly recommended when a possible leakage of the operating fluid in the environment is unacceptable.
- the back portion of the seals 10 ′ and 11 ′ abuts against corresponding countercheck elements 12 ′ and 13 ′, i.e. the seals are pushed in the opposed direction.
- the seals 10 ′ and 11 ′ and the corresponding countercheck elements 12 ′ and 13 ′ reciprocally move due to the rotary movement of the shaft.
- This is a configuration providing for an intermediate chamber 9 ′ between the bearings supporting the turbine shaft and the zone where the operating fluid expands.
- FIG. 4 shows another configuration provided by the regulation, this time of “face to face” type, where the seals are pushed against one another.
- the seals 10 ′, 11 ′ can axially slide so as to move in abutment at the respective front face against only one ring 14 ′ provided between the same seals themselves and having the countercheck elements 12 ′ and 13 ′ thereon.
- FIGS. 5, 5 a and 5 b are schematic views in axially symmetrical section of corresponding double-sealed arrangements used in traditional Rankine and not-organic ORC cycle turbines, which are particularly adapted to be used in case the shaft has, at the sliding surfaces, high rotation speed greater than 10 m/s.
- the solution shown in FIG. 5 is of “back to back” type, where the seals 10 ′ and 11 ′ are pushed in opposite directions by corresponding springs 15 ′ and 16 ′ towards the countercheck elements 12 ′ and 13 ′.
- the sealing is achieved at the S 1 and S 2 interface between the seal 10 ′ and the countercheck element 12 ′ and between the seal 11 ′ and the countercheck element 13 ′, respectively.
- a barrier liquid is fed through a feeding duct A′′, then is drained by several output ducts B′ and C′ which might also drain the barrier liquid possibly leaked through the interface S 1 , if the seal is not perfect.
- the flow of the mixture containing the possible flow rate of the barrier fluid able to cross the interface S 1 and part of the lubricating oil initially fed to the bearing 8 ′ is drained through the duct C′.
- the same operating fluid expanding in the turbine is fed through D′.
- FIG. 5 a shows a variation, equivalent to that shown in FIG. 5 , with the difference that the springs 15 ′ and 16 ′ have been replaced by metal bellows 15 ′′ and 16 ′′, being more resistant against high temperatures and abrasive action applied by the fluid contaminated by solid substances, for example particulate.
- FIG. 5 b is a variation substantially identical to that shown in FIG. 5 , but provided with an additional sleeve 17 ′ connected to the stationary portion of the turbine and provided with helical grooves which generate a fluid-dynamic pumping effect.
- the viscous friction of the fluid fed between the seals 10 ′ and 11 ′ exerts an action pumping on the fluid itself, in the way determined by the tilt of the helical grooves of the sleeve 17 ′. Due to the pumping effect, the barrier fluid is thrown against the base of the countercheck element 12 ′ in the form of jet, as denoted by the arrow in figure.
- Some embodiments provide that, in order to keep the seal faces separate from each other so as to prevent the relative wear, a minimum and controlled flow rate of barrier fluid leaks through the sealing surface.
- barrier fluids such as oil or water is problematic in ORC Rankine cycles, as these fluids, if there is a leakage flow to the ORC process, can contribute to thermal degradation of the organic operating fluid, facilitate sediment accumulation and, when present in large amounts in the plant, can interfere with the proper operation of the ORC Rankine cycle.
- Seals are arranged so as three or four chambers arranged in succession along and around the turbine shaft are defined and kept isolated.
- the organic operating fluid i.e. the same fluid fed to the turbine, is fed into one of the chambers, that is a buffer chamber, in this case with function of barrier fluid. In this way it is possible to guarantee both that the operating fluid is confined in the turbine and is not contaminated.
- the present invention in a first aspect thereof, relates to a turbine according to claim 1 of an organic Rankine cycle ORC.
- the proposed solution being set out in a plurality of seal arrangements, simultaneously guarantees to effectively confine the operating fluid in the Rankine cycle ORC, without any possibility of being contaminated by the lubricant of the turbine bearings, and to protect the environment due to the fact that the operating fluid leaked from an intermediate seal joins a flow of preferably inert gas and can be quite easily separated therefrom before releasing the latter in the atmosphere.
- a second aspect of the present invention concerns a method according to claim 16 for confining the operating fluid in a turbine working in an organic Rankine cycle ORC and for preventing any leakages into the surrounding environment.
- a further aspect of the present invention relates to a plant according to one of claims 25 - 27 .
- FIG. 1 is a schematic view in axially symmetrical section of a solution sealed between the turbine and the generator, according to the known art
- FIG. 2 is a schematic view in axially symmetrical section of another sealed arrangement according to the known art
- FIG. 3 is a schematic view of an arrangement of seals according to ANSI/API regulation
- FIG. 4 is a schematic view of another arrangement of seals according to ANSI/API regulation
- FIG. 5 is a schematic view in axially symmetrical section of an arrangement of seals in a turbine, according to the known art
- FIG. 5 a is a schematic view in axially symmetrical section of a variation of the seals arrangement shown in FIG. 5 ;
- FIG. 5 b is a schematic view in axially symmetrical section of a variation of the seal arrangement shown in FIG. 5 ;
- FIG. 6 is a conceptual diagram of a Rankine cycle ORC
- FIG. 7 is a schematic view, partially in axially symmetrical section, of a Rankine Cycle ORC turbine
- FIG. 8 is a diagram of a first arrangement of seals according to the present invention.
- FIG. 9 is a diagram of a second arrangement of seals according to the present invention.
- FIG. 10 is a diagram of a third arrangement of seals according to the present invention.
- FIG. 11 is a diagram of a fourth arrangement of seals according to the present invention.
- FIG. 12 is a diagram of a fifth arrangement of seals according to the present invention.
- FIG. 13 is a diagram of a Rankine cycle ORC plant according to the present invention.
- FIGS. 1-5 b relate to solutions according to known art, wherein the generator is sealed with a double seal in a “back to back” and “face to face” configuration, and the respective description is provided at the beginning of the text.
- FIG. 6 a diagram of a typical Rankine cycle ORC is shown.
- the numeral reference 1 indicates an evaporator combined with a heat source.
- a turbine assembly and the respective electric generator 4 are schematically shown in the dotted circle 2 .
- a regenerator 5 having the outlet of the turbine 3 connected thereto, can be present or absent.
- the numeral reference 6 denotes a condenser combined with a cold source and the numeral reference 7 denotes a feeding pump.
- FIG. 7 schematically shows a partial sectional view of the turbine 3 shown in the box 2 of FIG. 6 .
- the turbine 3 comprises a shaft 8 supported by the bearings 9 and 10 on the rotation axis X-X.
- a volute 11 and a holder-sleeve bearing 12 define the stationary portion.
- a supporting disc 13 is constrained to the shaft 8 and holds the rotor blades 14 ; the latter, together with the stator blades 15 supported by the stationary portion, constitute a stage of the turbine 3 .
- the arrows respectively denote the input of the operating fluid in the volute 11 and the output of the (expanded) fluid to the regenerator.
- the seals of the turbine in this figure schematically shown by the rectangle 16 , are provided between the bearings 9 and 10 and the supporting disc 13 (and therefore the expanding stage).
- the seals must prevent the operating fluid expanding in the turbine from flowing towards the bearings 9 and 10 and also prevent contaminants, such as the lubricating oil of the bearings, from mixing with the operating fluid in the expansion stage.
- the seals can be arranged in accordance with to ‘back to back’, ‘face to face’, or ‘face-to-back’ schemes, depending on the designer's choice.
- FIGS. 8 to 12 are schematic views of corresponding seal arrangements according to the present invention.
- seals extend circumferentially around the shaft and are coaxial thereto.
- Numeral reference 101 indicates a circumferential cooling chamber in which a coolant flows.
- Chambers 100 - 500 are separated by suitable ring-shaped elastic seals.
- the seals are defined by rings having O-rings fitted both on their inner and outer diameters.
- the seal rings can be in positions different from the position shown in the accompanying figures, still remaining within the scope of the present invention.
- sub-chamber 100 and the chamber 50 are not separated by seals, but by a labyrinth 50 b.
- Operating fluid i.e. the same fluid expanding through the stage of the turbine 3
- p 200 The pressure of the operating fluid in the chamber 200 is denoted by p 200 .
- a flow rate of the operating fluid is withdrawn from the sub-chamber 100 , if present, by means of outlet channels A′ and can be delivered (preferably) to the condenser.
- the pressure of the operating fluid in the chamber 100 is denoted by p 100 .
- the pressure is denoted by p 50 and typically corresponds to the exhaust pressure from the turbine, although pressure losses through the balancing holes and the effects of a possible diffuser at the outlet of the turbine must be considered.
- a preferably inert gas such as nitrogen N 2 or argon Ar or carbon dioxide CO 2 , is fed into the chamber 400 by means of inflow channels; otherwise, in order to keep the pressure values given below, filtered air is fed; although air is not considered as an inert gas, for the above mentioned purposes it can be considered, to a good approximation, to be similar.
- inert gas such as nitrogen N 2 or argon Ar or carbon dioxide CO 2
- the inert gas is selected so as to have a minimum solubility in the operating fluid in liquid phase.
- a solubility threshold that can be considered is 1000 PPM if there is 20° C. liquid subcooling with respect to the saturation temperature.
- the seals T 5 -T 8 are gas seals, known as ‘dry gas seals’.
- the seal rings are made of silicon carbide, or silicon or carbon nitride.
- the rings of the gas seals contact each other and when the turbine rotates they move away (by few microns, actually): the gas flows from the higher pressure chamber to the lower pressure one, with a flow rate being a function of the pressure difference, the geometry of the rings, the rotation speed, the distance between the rings.
- the surface of the seal rings is preferably coated with diamond powder bound with a suitable binder (e.g. sintered cobalt), or with sintered diamond, so as to provide high thermal conductivity and surface hardness.
- a suitable binder e.g. sintered cobalt
- the operating fluid injected into the buffer chamber 200 as barrier fluid may flow at most in the chamber 50 (through the sub-chamber 100 , if present) and from there back to the process.
- the fluid that can accumulate in the chamber 300 can be operating fluid, inert gas or a mixture of the two.
- the mixture withdrawn by the ducts B is delivered to a processing plant for recovering the operating fluid, i.e. to decontaminate it from the inert gas.
- the arrows show the direction of the flows through the seals.
- pressures are selected so that, in working conditions:
- P saturation means the vapor pressure of the barrier fluid at the adduction temperature in the chamber 200 .
- the condition (6) ensures that the direction of flow can be only from the chamber 200 to the chamber 300 .
- the conditions (7) and (8), together, ensure that no lubricant can flow from the bearings 9 , 10 to the chamber 300 .
- the leakage of operating fluid through the seals T 1 and T 2 must be greater than or equal to 0.2 cu ⁇ cm/hour per centimeter of the inner perimeter of the seal ring T 1 .
- Metal bellows can be used in place of the elastic elements 17 , i.e. the springs.
- FIG. 9 shows a second configuration.
- eight seal rings T 1 -T 8 are provided, although in this case the seals T 1 , T 4 , T 5 and T 8 do not rotate together with the shaft 8 whereas the seals T 2 , T 3 , T 6 and T 7 rotate together with the shaft 8 .
- the seals T 1 , T 4 , T 5 and T 8 are axially pushed towards the corresponding seals T 1 , T 4 , T 5 and T 8 by the action of the elastic elements. If the seals T 2 , T 3 , T 6 and T 7 must rotate at high speed, this configuration is preferable.
- At least the seals T 5 -T 6 , T 7 -T 8 , or even the seals T 1 -T 2 and T 3 -T 4 are equivalent to those described in U.S. Pat. No. 3,819,191. They are rings generating a radial seal against the outer surface of the turbine shaft and a side seal with respect to a complementary stationary ring.
- the single chamber 300 of the above described solutions is herein divided in two chambers 301 and 302 .
- Operating fluid is fed into the buffer chamber 200 by means of inflow channels A to function as barrier fluid; recovered operating fluid is withdrawn from the sub-chamber 100 , if present, by means of outlet channels A′. If there isn't the sub-chamber 100 , the leaked fluid directly flows to the chamber 50 .
- Gas preferably inert and preferably nitrogen N 2 , is fed into the chamber 400 through inflow channels C. If the inert gas is able to pass through the seals dividing the chambers 400 and 500 , then it is withdrawn from the chamber 500 .
- the mixture of inert gas and operating fluid is withdrawn from the chamber 301 through discharge outlets B; the inert gas could pass from the chamber 302 to the chamber 301 through the gaps between the labyrinth element 121 and the bushing 81 , whereas the operating fluid, in liquid or aeriform phase, could reach the chamber 301 leaking through the seals that separate this chamber from the buffer chamber 200 .
- FIG. 11 shows another configuration.
- the gas seals are those corresponding to the rings T 5 -T 8 .
- the seals corresponding to T 1 -T 4 are rings in the front-to-back configuration.
- FIG. 12 shows another seal arrangement according to the present invention, in which the seal rings T 8 and T 9 of the gas type are radially arranged on different diameters in order to reduce the overall axial dimension of the seal assembly 16 .
- the inert gas injected into the chamber 400 through the ducts C can pass at most into the chamber 500 through the seals T 8 and T 6 , and into the chamber 300 through the seals T 7 and T 6 .
- the operating fluid injected into the buffer chamber 200 can pass at most into the chamber 300 through the seals T 4 and T 5 , and into the chamber 100 through the seals T 3 and T 2 .
- a mixture of inert gas and operating fluid can therefore be formed in the chamber 300 , as described in the previous examples.
- the separate rings T 7 and T 8 can be effectively replaced by a single ring being fed at an intermediate position through the channel C.
- FIG. 13 shows an exemplary plant to recover the operating fluid, i.e. to separate the operating fluid from any contaminants; additional components with respect to a simple Rankine cycle ORC plant can be found out by a comparison with FIG. 6 .
- the numeral reference 18 indicates two filters arranged along the line conveying the operating fluid in liquid phase from the condenser, preferably downstream of the feeding pump 7 , to the inflow channels A of the seal zone 16 (only schematically shown in this figure), i.e. to the buffer chamber 200 in order to act as barrier fluid.
- a pump 7 ′ is provided along the line.
- filters 18 There are two filters 18 , because the upstream one protects the pump from possible solid particulate, the downstream one purifies from the fine particulate (range of 1-5 micrometers) and the possible water present therein.
- the filters are preferably redundant in pairs, to allow for cleaning without having to stop the process.
- a relief valve 19 is designed to vent the operating fluid towards the condenser 6 when a threshold pressure is exceeded, the latter being set so that the barrier fluid is properly fed to the chamber 200 .
- the valve 19 is connected to a line 471 conveying the operating fluid from the outlet A′ to the condenser 6 .
- the pressure P 300 is adjusted by acting on the rotation speed of the motor 24 .
- the unit 22 is provided with a chiller 27 to cool the mixture, at inlet temperatures preferably comprised between ⁇ 20° C. and +10° C., and with coalescent filters 28 intercepting the operating fluid.
- the fluid is separated from the inert gas by a low temperature condensation: at the processing temperatures, one of the mixture components is condensible, whereas the other is gaseous.
- the fraction of inert gas separated from the operating fluid is vented in the atmosphere through a vent pipe 26 preferably provided with an activated carbon filter.
- the relief valve 25 keeps under control the upstream pressure along the line.
- the decontaminated operating fluid is delivered to the valve 21 and then again to the condenser 6 , to be completely recovered.
- the abbreviation PC denotes the pressure control ruled by the valve; the abbreviation LC denotes the liquid flow rate control ruled by the valve.
- the numeral references 20 and 20 ′ indicate corresponding one-way valves.
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Abstract
Description
- The present invention relates to a seal arrangement in a turbine working in an Organic Rankine Cycle (ORC), and a method for confining the operating fluid in the turbine.
- The abbreviation ORC “Organic Rankine Cycle” usually denotes thermodynamic cycles of Rankine type that use an organic operating fluid preferably provided with high molecular mass, much higher than that of the water vapor used by the vast majority of the Rankine power cycles.
- The term ORC Organic Rankine Cycle has been used also to denote cycles with changes of state from liquid to gaseous and vice versa, even with operating fluids other than water, though not “organic” in the strict sense of “containing carbon”. For example, ammonia and nitrogen oxides are fluids having these characteristics.
- In the plants exploiting this thermodynamic cycle, in order to generate the heat required for vaporizing the organic operating fluid, biomass or waste heats of industrial processes is often used. The operating fluid is expanded in a turbine generally connected to an electric generator for producing electric power.
- In most of the Rankine cycle ORC plants, the organic operating fluid must necessarily remain confined in the plant, in order to prevent atmosphere contaminations. On the other hand, air must be prevented from entering the thermodynamic cycle, because oxygen would contribute to oxidation and corrosion of the organic operating fluid and, furthermore, the humidity in the air would pollute the operating fluid.
- In this sense, by confining the organic operating fluid, both the leakages of the latter in the surrounding environment and the input of air into the plant must be prevented.
- Typically, critical situations arise at interfaces among stationary portions and rotating shafts of the turbine. It is difficult to obtain effective seals for confining the turbine at such interfaces.
- Various technical solutions have been proposed.
-
FIG. 1 shows a classic solution according to the known art: theturbine 1′ andgenerator 2′ are directly coupled to each other and isolated inside acasing 3′. Theshaft 4′ of theturbine 1′ and thegenerator 2′ both rotate within the same volume defined by thevolute 3′ in which there is the operating fluid. Theshaft 4′ of the turbine does not cross the wall of thecasing 3′ thereby limiting only to the stationary seal the risk of leakages of the operating fluid. Electric power produced by the generator is transmitted to the outside through convenientelectrical connectors 5′ constrained to thevolute 3′ and being obviously fluid tight, to which corresponding cables can be connected. This solution suffers from the drawback of exposing the electric generator to the operating fluid. As the insulation of electric windings of thegenerator 2′ are continuously in contact with the operating fluid, in the long run it can be damaged and impaired. -
FIG. 2 shows an evolution of the previous solution, still according to the known art. The stator part and the rotor part of the generator are kept fluidically separated by acylindrical partition 6′, named liner, andgaskets 7′. - Both the solutions shown in
FIGS. 1 and 2 provide the use of agenerator 2′ specifically designed and sized. This involves higher costs and complications compared with the adoption of a standard type generator available on the market, which also provides higher average reliability. - Additionally, also the
bearings 8′ (schematically shown) supporting theshaft 4′ are exposed to the operating fluid, therefore the latter having to act also as lubricant and cooling fluid. The operating fluid is discharged through suitable ducts. As an alternative to this solution, radial and axial magnetic bearings have been proposed. - As a further drawback, in the gap between the stator and the rotor of the
electric generator 2′ there is operating fluid; regardless of whether the latter is in the liquid phase or vapor phase, high fluid-dynamic losses arise, certainly greater than those occurring in case the operating fluid is in the gaseous phase of a gas having low molecular mass, such as the air surrounding the rotor of a conventional generator. If there is theliner 6′, because of its bulk, the gap must be kept large, and this can lead not to obtain the maximum electrical efficiency for the generator, other conditions unchanged. - Furthermore, in the volume inside the
casing 3′ saturated by the operating fluid, the positioning of instruments, warning lights, indicators is hampered, both because of the potential damage to the instruments themselves and because connecting elements should cross the sealed casing. - Due to the described drawbacks, in the Rankine cycle ORC plants of medium and large size, from a few hundred kW to over 10 MW, oil-lubricated bearings for supporting the turbine shaft, and a suitable arrangement of fluidic seals to achieve the confinement of the operating fluid in the plant, are used. This solution allows to adopt electric generators of standard type, and it is also possible to introduce a reduction gear between the turbine and the generator thereby optimizing the number of revolutions of the turbine and the generator.
- Over the years, many configurations of the fluidic seals have been proposed, in order to achieve the confinement of the process fluid, especially in chemical plants and the oil & gas field. Many of these configurations are described in the ANSI/API regulation Std. 682 and Std. 617.
-
FIG. 3 shows one of the configurations provided by the regulation: it is a configuration called “Double seal” or “Tandem seal” of “back to back” type, particularly recommended when a possible leakage of the operating fluid in the environment is unacceptable. The back portion of theseals 10′ and 11′ abuts againstcorresponding countercheck elements 12′ and 13′, i.e. the seals are pushed in the opposed direction. Theseals 10′ and 11′ and thecorresponding countercheck elements 12′ and 13′ reciprocally move due to the rotary movement of the shaft. This is a configuration providing for anintermediate chamber 9′ between the bearings supporting the turbine shaft and the zone where the operating fluid expands. Only in the case of “Double seal”, which is the most effective solution to ensure the confinement in theintermediate chamber 9′ definable buffer chamber, the pressure of a sealing fluid, definable barrier fluid, is kept higher than the pressure of the operating fluid in the adjacent zone of the turbine. Typically, oil or water is used as barrier fluid. -
FIG. 4 shows another configuration provided by the regulation, this time of “face to face” type, where the seals are pushed against one another. Theseals 10′, 11′ can axially slide so as to move in abutment at the respective front face against only onering 14′ provided between the same seals themselves and having thecountercheck elements 12′ and 13′ thereon. -
FIGS. 5, 5 a and 5 b are schematic views in axially symmetrical section of corresponding double-sealed arrangements used in traditional Rankine and not-organic ORC cycle turbines, which are particularly adapted to be used in case the shaft has, at the sliding surfaces, high rotation speed greater than 10 m/s. - In particular, the solution shown in
FIG. 5 is of “back to back” type, where theseals 10′ and 11′ are pushed in opposite directions bycorresponding springs 15′ and 16′ towards thecountercheck elements 12′ and 13′. Clearly, the sealing is achieved at the S1 and S2 interface between theseal 10′ and thecountercheck element 12′ and between theseal 11′ and thecountercheck element 13′, respectively. - A barrier liquid is fed through a feeding duct A″, then is drained by several output ducts B′ and C′ which might also drain the barrier liquid possibly leaked through the interface S1, if the seal is not perfect. For example, the flow of the mixture containing the possible flow rate of the barrier fluid able to cross the interface S1 and part of the lubricating oil initially fed to the
bearing 8′, is drained through the duct C′. The same operating fluid expanding in the turbine is fed through D′. -
FIG. 5a shows a variation, equivalent to that shown inFIG. 5 , with the difference that thesprings 15′ and 16′ have been replaced bymetal bellows 15″ and 16″, being more resistant against high temperatures and abrasive action applied by the fluid contaminated by solid substances, for example particulate. -
FIG. 5b is a variation substantially identical to that shown inFIG. 5 , but provided with anadditional sleeve 17′ connected to the stationary portion of the turbine and provided with helical grooves which generate a fluid-dynamic pumping effect. The viscous friction of the fluid fed between theseals 10′ and 11′ exerts an action pumping on the fluid itself, in the way determined by the tilt of the helical grooves of thesleeve 17′. Due to the pumping effect, the barrier fluid is thrown against the base of thecountercheck element 12′ in the form of jet, as denoted by the arrow in figure. - Some embodiments provide that, in order to keep the seal faces separate from each other so as to prevent the relative wear, a minimum and controlled flow rate of barrier fluid leaks through the sealing surface.
- Often, solutions provided by the known art do not guarantee the effective confinement of the operating fluid if the latter is organic fluid, such as in Rankine cycles ORC, and the turbine rotates at very high speed, i.e. typically at speeds higher than 10 m/s next to the slide surfaces of the seals.
- Furthermore, adopting barrier fluids such as oil or water is problematic in ORC Rankine cycles, as these fluids, if there is a leakage flow to the ORC process, can contribute to thermal degradation of the organic operating fluid, facilitate sediment accumulation and, when present in large amounts in the plant, can interfere with the proper operation of the ORC Rankine cycle.
- The Italian Patent Applications BS2014A000159 and BS2014A000160, both filed Aug. 28, 2014 by the Applicant, describe corresponding seal arrangements able to solve the above described drawbacks. Seals are arranged so as three or four chambers arranged in succession along and around the turbine shaft are defined and kept isolated. The organic operating fluid, i.e. the same fluid fed to the turbine, is fed into one of the chambers, that is a buffer chamber, in this case with function of barrier fluid. In this way it is possible to guarantee both that the operating fluid is confined in the turbine and is not contaminated.
- The Applicant found that the just described solutions have the drawback that the operating fluid able to pass through the double seal, mixes with the air and oil coming from the zone of the bearings, thereby contaminating the oil. Therefore, the mixture has to be processed in order to separate the operating fluid and reuse the same.
- It is an object of the present invention to provide a Rankine cycle ORC turbine provided with a seal arrangement alternative to those described in the Italian Patent Applications BS2014A000159 and BS2014A000160, and anyway improved in order to achieve the effective confinement of the operating fluid and preventing it from being contaminated in any operative condition.
- Therefore the present invention, in a first aspect thereof, relates to a turbine according to
claim 1 of an organic Rankine cycle ORC. - The proposed solution, being set out in a plurality of seal arrangements, simultaneously guarantees to effectively confine the operating fluid in the Rankine cycle ORC, without any possibility of being contaminated by the lubricant of the turbine bearings, and to protect the environment due to the fact that the operating fluid leaked from an intermediate seal joins a flow of preferably inert gas and can be quite easily separated therefrom before releasing the latter in the atmosphere.
- Further preferred features of the turbine are described in the dependent claims 2-15.
- A second aspect of the present invention concerns a method according to claim 16 for confining the operating fluid in a turbine working in an organic Rankine cycle ORC and for preventing any leakages into the surrounding environment.
- Further preferred steps are described in claims 14-24.
- A further aspect of the present invention relates to a plant according to one of claims 25-27.
- However, further details of the invention will be evident from the following description made with reference to the attached figures, in which:
-
FIG. 1 is a schematic view in axially symmetrical section of a solution sealed between the turbine and the generator, according to the known art; -
FIG. 2 is a schematic view in axially symmetrical section of another sealed arrangement according to the known art; -
FIG. 3 is a schematic view of an arrangement of seals according to ANSI/API regulation; -
FIG. 4 is a schematic view of another arrangement of seals according to ANSI/API regulation; -
FIG. 5 is a schematic view in axially symmetrical section of an arrangement of seals in a turbine, according to the known art; -
FIG. 5a is a schematic view in axially symmetrical section of a variation of the seals arrangement shown inFIG. 5 ; -
FIG. 5b is a schematic view in axially symmetrical section of a variation of the seal arrangement shown inFIG. 5 ; -
FIG. 6 is a conceptual diagram of a Rankine cycle ORC; -
FIG. 7 is a schematic view, partially in axially symmetrical section, of a Rankine Cycle ORC turbine; -
FIG. 8 is a diagram of a first arrangement of seals according to the present invention; -
FIG. 9 is a diagram of a second arrangement of seals according to the present invention; -
FIG. 10 is a diagram of a third arrangement of seals according to the present invention; -
FIG. 11 is a diagram of a fourth arrangement of seals according to the present invention; -
FIG. 12 is a diagram of a fifth arrangement of seals according to the present invention; -
FIG. 13 is a diagram of a Rankine cycle ORC plant according to the present invention. -
FIGS. 1-5 b relate to solutions according to known art, wherein the generator is sealed with a double seal in a “back to back” and “face to face” configuration, and the respective description is provided at the beginning of the text. - Referring to
FIG. 6 , a diagram of a typical Rankine cycle ORC is shown. Thenumeral reference 1 indicates an evaporator combined with a heat source. A turbine assembly and the respectiveelectric generator 4 are schematically shown in thedotted circle 2. Depending on temperatures and characteristics of the operating fluid, aregenerator 5 having the outlet of theturbine 3 connected thereto, can be present or absent. Thenumeral reference 6 denotes a condenser combined with a cold source and thenumeral reference 7 denotes a feeding pump. -
FIG. 7 schematically shows a partial sectional view of theturbine 3 shown in thebox 2 ofFIG. 6 . - The
turbine 3 comprises ashaft 8 supported by thebearings volute 11 and a holder-sleeve bearing 12 define the stationary portion. A supportingdisc 13 is constrained to theshaft 8 and holds therotor blades 14; the latter, together with thestator blades 15 supported by the stationary portion, constitute a stage of theturbine 3. The arrows respectively denote the input of the operating fluid in thevolute 11 and the output of the (expanded) fluid to the regenerator. - The seals of the turbine, in this figure schematically shown by the
rectangle 16, are provided between thebearings - As mentioned, at the same time the seals must prevent the operating fluid expanding in the turbine from flowing towards the
bearings - Generally, the seals can be arranged in accordance with to ‘back to back’, ‘face to face’, or ‘face-to-back’ schemes, depending on the designer's choice.
-
FIGS. 8 to 12 are schematic views of corresponding seal arrangements according to the present invention. - It should be recalled that the seals extend circumferentially around the shaft and are coaxial thereto.
- Referring to the first example of
FIG. 8 , the following chambers, or rooms, are defined: -
-
chamber 50, also visible inFIG. 7 , corresponding to one of the inner rooms where the operating fluid making the ORC cycle flows. For example, thechamber 50 can be constituted by the room between thezone 16 of the seals and arotor disc 13. Preferably, thanks to balancingholes 473, the pressure inside thechamber 50 is equal to the exhaust pressure of the turbine. A fluid fed to this room is then drawn back and mixes with the general flow of operating fluid expanded in the turbine; -
chamber 500, also visible inFIG. 7 , corresponding to the room between thezone 16 of the seals and thebearings bearings -
chamber 200, named buffer chamber, immediately adjacent to thechamber 50 or adjacent to a sub-chamber 100, if present, on the opposite side with respect to the supportingdisc 13; -
chamber 400, immediately adjacent to thechamber 500 on the opposite side with respect to thebearings -
chamber 300 in-between thechambers - the sub-chamber 100, which is optional, obtained by dividing the
chamber 50 by means of aradial wall 50 a, for example provided with alabyrinth 50 b. Object of the sub-chamber 100, if present, is to withdraw at least one portion of the leaked fluid directly downstream of the seal defined by the rings T1 and T2. This function can be particularly useful when a high flow rate has leaked, in order to prevent this flow rate from being entirely delivered to the room of the turbine rotor, thus endangering the stability of the rotor itself. Moreover, if there is the sub-chamber 100, this has the function of receiving the leaked fluid in at least partially liquid phase, so that the collected fluid cools down the walls by gradual evaporation.
-
-
Numeral reference 101 indicates a circumferential cooling chamber in which a coolant flows. - Chambers 100-500 are separated by suitable ring-shaped elastic seals. It should be noted that figures schematically show the mutual position of the seals but not the respective assembly sequence. Therefore, in practice, the seals are defined by rings having O-rings fitted both on their inner and outer diameters. In order to optimally balance the rotating parts of the
turbine 3, the seal rings can be in positions different from the position shown in the accompanying figures, still remaining within the scope of the present invention. - In
FIG. 8 , where there is the sub-chamber 100, the following seal rings are shown: -
- the seal ring T1 is rotationally integral with the
bushing 81 of theshaft 8 and, therefore, the shaft itself. Anelastic element 17 pushes the ring T1 towards the corresponding stationary seal ring T2; - the seal ring T2 is integral with the stationary portion of the
turbine 3 and, therefore, does not rotate on the X-X axis; - the seal ring T3 is similar to the ring T2 but is positioned so as to interface with the seal ring T4;
- the seal ring T4 is rotationally integral with the
bushing 81 of theshaft 8 and, therefore, the shaft itself. Anelastic element 17 pushes the ring T4 towards the corresponding stationary seal ring T3; - the seal ring T5 is rotationally integral with the
bushing 81 of theshaft 8 and, therefore, the shaft itself. Anelastic element 17 pushes the ring T1 towards the corresponding stationary seal ring T6; - the seal ring T6 is integral with the stationary portion of the
turbine 3 and, therefore, does not rotate on the X-X axis; - the seal ring T7 is similar to the ring T6 but is positioned so as to interface with the seal ring T8;
- the seal ring T8 is rotationally integral with the
bushing 81 of theshaft 8 and, therefore, the shaft itself. Anelastic element 17 pushes the ring T8 towards the corresponding stationary seal ring T7.
- the seal ring T1 is rotationally integral with the
- It should be noted that the sub-chamber 100 and the
chamber 50 are not separated by seals, but by alabyrinth 50 b. - Once the seal rings are in abutment each against the corresponding ring (actually the distance is in the range 1-10 microns), a barrier obstructing the fluid passage is created.
- Operating fluid, i.e. the same fluid expanding through the stage of the
turbine 3, is fed into thechamber 200 by means of inflow channels A. The pressure of the operating fluid in thechamber 200 is denoted by p200. - A flow rate of the operating fluid is withdrawn from the sub-chamber 100, if present, by means of outlet channels A′ and can be delivered (preferably) to the condenser. The pressure of the operating fluid in the
chamber 100 is denoted by p100. - In the
chamber 50 the pressure is denoted by p50 and typically corresponds to the exhaust pressure from the turbine, although pressure losses through the balancing holes and the effects of a possible diffuser at the outlet of the turbine must be considered. - Due to the leakage through the seals T5/T6 and T3/T4, fluid may accumulate in the
chamber 300 and is withdrawn therefrom by means of outlet channels B. In thechamber 300, the pressure is denoted by p300. - A preferably inert gas, such as nitrogen N2 or argon Ar or carbon dioxide CO2, is fed into the
chamber 400 by means of inflow channels; otherwise, in order to keep the pressure values given below, filtered air is fed; although air is not considered as an inert gas, for the above mentioned purposes it can be considered, to a good approximation, to be similar. - Preferably, the inert gas is selected so as to have a minimum solubility in the operating fluid in liquid phase. For example, a solubility threshold that can be considered is 1000 PPM if there is 20° C. liquid subcooling with respect to the saturation temperature.
- In the
chamber 400, the gas pressure is denoted by p400. Therefore, the seals T5-T8 are gas seals, known as ‘dry gas seals’. Preferably, the seal rings are made of silicon carbide, or silicon or carbon nitride. - When the
turbine 3 is stationary, the rings of the gas seals contact each other and when the turbine rotates they move away (by few microns, actually): the gas flows from the higher pressure chamber to the lower pressure one, with a flow rate being a function of the pressure difference, the geometry of the rings, the rotation speed, the distance between the rings. - The surface of the seal rings, designed to come in contact with another seal ring, is preferably coated with diamond powder bound with a suitable binder (e.g. sintered cobalt), or with sintered diamond, so as to provide high thermal conductivity and surface hardness.
- In practice, by keeping the following pressure conditions:
-
p 300 <p 200 (1) -
p 50 <p 200 (2) -
p 300 <p 400 (3) -
p 500 <p 400. (4) - an optimal confinement of the operating fluid in the
turbine 3 is achieved. - If there is the sub-chamber 100, along with the above listed conditions, it is also required to keep the following condition: p200>P100>p50.
- If the seal defined by the rings T1 and T2 does not completely prevent the passage of fluid, the operating fluid injected into the
buffer chamber 200 as barrier fluid may flow at most in the chamber 50 (through the sub-chamber 100, if present) and from there back to the process. - If the seal defined by the rings T3 and T4 does not completely prevent the passage of fluid, a portion of the operating fluid injected into the
buffer chamber 200 as barrier fluid can flow into thechamber 300 where it can mix with the gas possibly passed through the seal defined by the rings T5 and T6. - If the seal defined by the rings T3 and T4 does not completely prevent the passage of gas, a portion of gas will leak into the
chamber 500 towards thebearings - The fluid that can accumulate in the
chamber 300 can be operating fluid, inert gas or a mixture of the two. In the latter case, the mixture withdrawn by the ducts B is delivered to a processing plant for recovering the operating fluid, i.e. to decontaminate it from the inert gas. - The arrows show the direction of the flows through the seals.
- Preferably pressures are selected so that, in working conditions:
-
2<p 400<4 bar, (absolute pressure), (5) -
p 300 ≤p 200−30000 Pa, (6) -
p 400 ≥p 300+20000 Pa, (7) -
p 400 ≥p 500+20000 Pa, (8) -
P 200 >P saturation+100000 Pa (9) - wherein Psaturation means the vapor pressure of the barrier fluid at the adduction temperature in the
chamber 200. - The condition (6) ensures that the direction of flow can be only from the
chamber 200 to thechamber 300. The conditions (7) and (8), together, ensure that no lubricant can flow from thebearings chamber 300. - Preferably, the leakage of operating fluid through the seals T1 and T2 must be greater than or equal to 0.2 cu·cm/hour per centimeter of the inner perimeter of the seal ring T1.
- In the condition in which the
first chamber 50 and thebuffer chamber 200 are adjacent, without interposition of the sub-chamber 100, it is preferable that: -
P 200 >P 50+80000 Pa. (11) - Metal bellows can be used in place of the
elastic elements 17, i.e. the springs. -
FIG. 9 shows a second configuration. As in the previous configuration, eight seal rings T1-T8 are provided, although in this case the seals T1, T4, T5 and T8 do not rotate together with theshaft 8 whereas the seals T2, T3, T6 and T7 rotate together with theshaft 8. The seals T1, T4, T5 and T8 are axially pushed towards the corresponding seals T1, T4, T5 and T8 by the action of the elastic elements. If the seals T2, T3, T6 and T7 must rotate at high speed, this configuration is preferable. - In an embodiment, at least the seals T5-T6, T7-T8, or even the seals T1-T2 and T3-T4, are equivalent to those described in U.S. Pat. No. 3,819,191. They are rings generating a radial seal against the outer surface of the turbine shaft and a side seal with respect to a complementary stationary ring.
- In the configuration shown in
FIG. 10 there is alabyrinth element 121. Therefore, thesingle chamber 300 of the above described solutions is herein divided in twochambers buffer chamber 200 by means of inflow channels A to function as barrier fluid; recovered operating fluid is withdrawn from the sub-chamber 100, if present, by means of outlet channels A′. If there isn't the sub-chamber 100, the leaked fluid directly flows to thechamber 50. Gas, preferably inert and preferably nitrogen N2, is fed into thechamber 400 through inflow channels C. If the inert gas is able to pass through the seals dividing thechambers chamber 500. The inert gas which may pass through the seals dividing thechambers chamber 302 through discharge outlets C′. The mixture of inert gas and operating fluid is withdrawn from thechamber 301 through discharge outlets B; the inert gas could pass from thechamber 302 to thechamber 301 through the gaps between thelabyrinth element 121 and thebushing 81, whereas the operating fluid, in liquid or aeriform phase, could reach thechamber 301 leaking through the seals that separate this chamber from thebuffer chamber 200. The advantage of this configuration is that, if inert gas is present in thechamber 302, it can be ejected into the atmosphere (only if P302>P301 is verified by suitably measuring the two values) and only a fraction passes into thechamber 301. Also in this case, the mixture withdrawn by the channels B must be processed to separate the inert gas from the operating fluid. -
FIG. 11 shows another configuration. The gas seals are those corresponding to the rings T5-T8. The seals corresponding to T1-T4 are rings in the front-to-back configuration. -
FIG. 12 shows another seal arrangement according to the present invention, in which the seal rings T8 and T9 of the gas type are radially arranged on different diameters in order to reduce the overall axial dimension of theseal assembly 16. The inert gas injected into thechamber 400 through the ducts C can pass at most into thechamber 500 through the seals T8 and T6, and into thechamber 300 through the seals T7 and T6. The operating fluid injected into thebuffer chamber 200 can pass at most into thechamber 300 through the seals T4 and T5, and into thechamber 100 through the seals T3 and T2. A mixture of inert gas and operating fluid can therefore be formed in thechamber 300, as described in the previous examples. - The separate rings T7 and T8 can be effectively replaced by a single ring being fed at an intermediate position through the channel C.
-
FIG. 13 shows an exemplary plant to recover the operating fluid, i.e. to separate the operating fluid from any contaminants; additional components with respect to a simple Rankine cycle ORC plant can be found out by a comparison withFIG. 6 . - The
numeral reference 18 indicates two filters arranged along the line conveying the operating fluid in liquid phase from the condenser, preferably downstream of thefeeding pump 7, to the inflow channels A of the seal zone 16 (only schematically shown in this figure), i.e. to thebuffer chamber 200 in order to act as barrier fluid. Along the line apump 7′ is provided. - There are two
filters 18, because the upstream one protects the pump from possible solid particulate, the downstream one purifies from the fine particulate (range of 1-5 micrometers) and the possible water present therein. The filters are preferably redundant in pairs, to allow for cleaning without having to stop the process. - A
relief valve 19 is designed to vent the operating fluid towards thecondenser 6 when a threshold pressure is exceeded, the latter being set so that the barrier fluid is properly fed to thechamber 200. Thevalve 19 is connected to aline 471 conveying the operating fluid from the outlet A′ to thecondenser 6. - The mixture withdrawn from the
chamber 300 through the outlet ducts B, and comprising operating fluid and inert gas, is compressed in thecompressor 23 driven by theelectric motor 24, and delivered to theunit 22. - Preferably, the pressure P300 is adjusted by acting on the rotation speed of the
motor 24. - The
unit 22 is provided with achiller 27 to cool the mixture, at inlet temperatures preferably comprised between −20° C. and +10° C., and withcoalescent filters 28 intercepting the operating fluid. In practice, the fluid is separated from the inert gas by a low temperature condensation: at the processing temperatures, one of the mixture components is condensible, whereas the other is gaseous. The fraction of inert gas separated from the operating fluid is vented in the atmosphere through avent pipe 26 preferably provided with an activated carbon filter. Therelief valve 25 keeps under control the upstream pressure along the line. - The decontaminated operating fluid is delivered to the
valve 21 and then again to thecondenser 6, to be completely recovered. The abbreviation PC denotes the pressure control ruled by the valve; the abbreviation LC denotes the liquid flow rate control ruled by the valve. - The numeral references 20 and 20′ indicate corresponding one-way valves.
Claims (27)
P 200 >P 100+40000 Pa. (11)
P 300 <P 200 (1)
P 50 <P 200 (2)
P 300 <P 400 (3)
P 500 <P 400. (4)
2<P 400<4 bar, (5)
P 300 ≤P 200−30000 Pa, (6)
P 400 ≥P 300+20000 Pa, (7)
P 400 ≥P 500+20000 Pa, (8)
P 200 >P saturation+100000 Pa (9)
P 200 >P 50+80000 Pa. (10)
P 200 >P 100+40000 Pa. (11)
P 300 <P 200 (1)
P 50 <P 200 (2)
P 300 <P 400 (3)
P 500 <P 400. (4)
2<P 400<4 bar, (5)
P 300 ≤P 200−30000 Pa, (6)
P 400 ≥P 300+20000 Pa, (7)
P 400 ≥P 500+20000 Pa, (8)
P 200 >P saturation+100000 Pa (9)
P 200 >P 50+80000 Pa. (10)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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IT102015000026784 | 2015-06-23 | ||
ITUB20151595 | 2015-06-23 | ||
PCT/IB2016/053365 WO2016207761A1 (en) | 2015-06-23 | 2016-06-08 | Seal arrangement in a turbine and method for confining the operating fluid |
Publications (2)
Publication Number | Publication Date |
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US20180187566A1 true US20180187566A1 (en) | 2018-07-05 |
US10344608B2 US10344608B2 (en) | 2019-07-09 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US15/738,304 Active 2036-06-17 US10344608B2 (en) | 2015-06-23 | 2016-06-08 | Seal arrangement in a turbine and method for confining the operating fluid |
Country Status (4)
Country | Link |
---|---|
US (1) | US10344608B2 (en) |
EP (1) | EP3314094B1 (en) |
CA (1) | CA2983902C (en) |
WO (1) | WO2016207761A1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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US20180328211A1 (en) * | 2015-10-22 | 2018-11-15 | Man Diesel & Turbo Se | Dry Gas Seal And Turbomachine Having A Dry Gas Seal |
CN110030046A (en) * | 2019-03-28 | 2019-07-19 | 华电电力科学研究院有限公司 | A kind of condensate system and operation method for Turbo-generator Set |
US10662798B2 (en) | 2015-10-22 | 2020-05-26 | Man Energy Solutions Se | Dry gas sealing system, and turbomachine comprising a dry gas sealing system |
US20220213828A1 (en) * | 2021-01-04 | 2022-07-07 | Volvo Car Corporation | Expander system |
IT202100002366A1 (en) * | 2021-02-03 | 2022-08-03 | Nuovo Pignone Tecnologie Srl | GLAND CONDENSER SKID SYSTEMS BY DIRECT CONTACT HEAT EXCHANGER TECHNOLOGY |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
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DE102017109663A1 (en) | 2017-05-05 | 2018-11-08 | Man Diesel & Turbo Se | Sealing system, turbomachine with a sealing system and method of cleaning the same |
FR3081512B1 (en) * | 2018-05-28 | 2021-06-04 | Safran Aircraft Engines | LARGE DISPLACEMENT SEALING DEVICE FOR AN AIRCRAFT ENGINE |
EP3575641A1 (en) * | 2018-05-30 | 2019-12-04 | Siemens Aktiengesellschaft | Arrangement, in particular turbomachine, comprising a shaft seal arrangement |
US11927105B1 (en) | 2022-09-16 | 2024-03-12 | General Electric Company | Thrust bearings to support axial thrust in pumps |
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US4005580A (en) * | 1975-06-12 | 1977-02-01 | Swearingen Judson S | Seal system and method |
US4484753A (en) * | 1983-01-31 | 1984-11-27 | Nl Industries, Inc. | Rotary shaft seal |
US5267736A (en) * | 1990-09-05 | 1993-12-07 | Blohm & Voss Ag | Sealing apparatus for rotating shafts, in particular stern tube seal for the propeller shaft of a ship |
US7249768B2 (en) * | 2004-05-07 | 2007-07-31 | United Technologies Corporation | Shaft seal assembly and method |
DE102007037311B4 (en) * | 2007-08-08 | 2009-07-09 | GMK Gesellschaft für Motoren und Kraftanlagen mbH | Shaft seal for a turbine for an ORC system, ORC system with such a turbine shaft seal and method for operating an ORC system |
IT1400729B1 (en) * | 2010-07-08 | 2013-07-02 | Turboden Srl | FLUID SEALING DEVICE FOR ROTATING MACHINES. |
US8915708B2 (en) * | 2011-06-24 | 2014-12-23 | Caterpillar Inc. | Turbocharger with air buffer seal |
-
2016
- 2016-06-08 US US15/738,304 patent/US10344608B2/en active Active
- 2016-06-08 EP EP16739559.9A patent/EP3314094B1/en active Active
- 2016-06-08 CA CA2983902A patent/CA2983902C/en active Active
- 2016-06-08 WO PCT/IB2016/053365 patent/WO2016207761A1/en unknown
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20180328211A1 (en) * | 2015-10-22 | 2018-11-15 | Man Diesel & Turbo Se | Dry Gas Seal And Turbomachine Having A Dry Gas Seal |
US10662798B2 (en) | 2015-10-22 | 2020-05-26 | Man Energy Solutions Se | Dry gas sealing system, and turbomachine comprising a dry gas sealing system |
CN110030046A (en) * | 2019-03-28 | 2019-07-19 | 华电电力科学研究院有限公司 | A kind of condensate system and operation method for Turbo-generator Set |
US20220213828A1 (en) * | 2021-01-04 | 2022-07-07 | Volvo Car Corporation | Expander system |
US11767784B2 (en) * | 2021-01-04 | 2023-09-26 | Volvo Car Corporation | Expander system |
IT202100002366A1 (en) * | 2021-02-03 | 2022-08-03 | Nuovo Pignone Tecnologie Srl | GLAND CONDENSER SKID SYSTEMS BY DIRECT CONTACT HEAT EXCHANGER TECHNOLOGY |
WO2022167148A1 (en) * | 2021-02-03 | 2022-08-11 | Nuovo Pignone Tecnologie - S.R.L. | Gland condenser skid systems by direct contact heat exchanger technology |
Also Published As
Publication number | Publication date |
---|---|
CA2983902C (en) | 2023-07-25 |
WO2016207761A1 (en) | 2016-12-29 |
CA2983902A1 (en) | 2016-12-29 |
US10344608B2 (en) | 2019-07-09 |
EP3314094A1 (en) | 2018-05-02 |
EP3314094B1 (en) | 2018-10-03 |
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